JPH05123200A - Preparation of galactooligosaccharide - Google Patents
Preparation of galactooligosaccharideInfo
- Publication number
- JPH05123200A JPH05123200A JP3321383A JP32138391A JPH05123200A JP H05123200 A JPH05123200 A JP H05123200A JP 3321383 A JP3321383 A JP 3321383A JP 32138391 A JP32138391 A JP 32138391A JP H05123200 A JPH05123200 A JP H05123200A
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- oligosaccharides
- hypocotyl
- soybean
- extract
- amount
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Abstract
(57)【要約】
【目的】 産業廃棄物である大豆胚軸から、有利にオリ
ゴ糖を抽出する方法を提供する。
【構成】 大豆種子の胚軸を原料とし、これをpH3乃至
6の酸性水溶液下に混合・攪拌して、ラフィノース、ス
タキオース等のオリゴ糖を抽出することを特徴とする、
ガラクトオリゴ糖の調製法。
【効果】 最近の豆腐製造時に副産物として発生する、
殆ど廃棄処分されてきた大豆の胚軸から有利にオリゴ糖
を抽出することができるという効果を有し、産業廃棄物
である大豆胚軸を有効に利用し得るという効果を有する
のである。(57) [Summary] [Objective] To provide a method for advantageously extracting oligosaccharides from soybean hypocotyl, which is industrial waste. [Structure] Soybean seed hypocotyl is used as a raw material, and this is mixed and stirred in an acidic aqueous solution of pH 3 to 6 to extract oligosaccharides such as raffinose and stachyose.
Method for preparing galactooligosaccharide. [Effect] It is generated as a by-product during the recent tofu production,
This has the effect that oligosaccharides can be advantageously extracted from the hypocotyl of soybeans that have been mostly disposed of, and that soybean hypocotyl, which is an industrial waste, can be effectively used.
Description
【0001】[0001]
【産業上の利用分野】本発明はガラクトオリゴ糖の調製
法に関し、特に従来より大豆の処理に際し副産物として
発生する胚軸を原料として、安価且つ簡便なガラクトオ
リゴ糖を調製法する方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for preparing a galacto-oligosaccharide, and more particularly to a method for preparing an inexpensive and simple galacto-oligosaccharide using hypocotyl, which has been conventionally generated as a by-product during soybean treatment.
【0002】[0002]
【従来の技術】従来より、人の腸内細菌の中でその整腸
効果が良いとされているビフィズス菌の活性因子として
多くのオリゴ糖が知られている。このビフィズス菌に資
化されるオリゴ糖はその分子量が5乃至6糖以下が良い
とされており、これらのオリゴ糖の中でも大豆から抽出
されるガラクトオリゴ糖、即ちラフィノース、スタキオ
ース等は一般に他のオリゴ糖よりもその活性が高いと言
われている。2. Description of the Related Art Conventionally, many oligosaccharides are known as active factors of bifidobacteria, which are said to have good intestinal-regulating effects among human intestinal bacteria. It is said that the oligosaccharides assimilated by Bifidobacteria have a molecular weight of 5 to 6 or less, and among these oligosaccharides, galactooligosaccharides extracted from soybean, that is, raffinose and stachyose are generally other oligosaccharides. It is said that its activity is higher than that of sugar.
【0003】ところで、大豆の胚軸は最近の豆腐製造時
に副産物として発生するが、これの有効利用は殆どなさ
れておらず、通常は廃棄処分されている。今後、この様
に副産物として発生する胚軸は豆腐の製造量が増すにつ
れ増加する事は必至である。By the way, the hypocotyl of soybean is generated as a by-product in the recent production of tofu, but it has not been effectively used and is normally discarded. In the future, it is inevitable that the hypocotyl generated as a by-product will increase as the production amount of tofu increases.
【0004】大豆中のオリゴ糖を抽出する方法は種々提
案されており、例えば特開昭59-179064 号発明または特
開昭60-66978号公報発明の如く、水を用いて抽出する場
合は一度大豆或いは脱脂大豆より豆乳を作成し、その豆
乳中に存在する蛋白質を沈殿除去してオリゴ糖を調製し
ている。また、特開昭62-155082 号発明では大豆を脱脂
後、20乃至60%のエタノール水溶液を用いてオリゴ糖を
抽出している。さらにまた、アルコール濃縮大豆蛋白質
製造時に副産物として生ずるホエイにオリゴ糖が多く含
有されていることから、このホエイからの抽出も行われ
ている。Various methods have been proposed for extracting oligosaccharides from soybeans. For example, as in the inventions of JP-A-59-179064 and JP-A-60-66978, once extraction is performed using water, Soy milk is prepared from soybeans or defatted soybeans, and proteins present in the soy milk are removed by precipitation to prepare oligosaccharides. Further, in Japanese Patent Application Laid-Open No. 62-155082, soybeans are defatted and then oligosaccharides are extracted using a 20 to 60% ethanol aqueous solution. Furthermore, since a large amount of oligosaccharides is contained in whey produced as a by-product during the production of alcohol-enriched soybean protein, extraction from this whey is also performed.
【0005】しかしながら、このような方法では、不純
物の除去やエタノールの処理にコストが掛かり繁雑であ
って安価なオリゴ糖を得難い。また、これまでに大豆の
胚軸よりオリゴ糖を抽出したという例はない。However, in such a method, removal of impurities and treatment of ethanol are costly and complicated, and it is difficult to obtain inexpensive oligosaccharides. In addition, there has been no example of extracting oligosaccharide from soybean hypocotyl.
【0006】[0006]
【発明が解決しようとする課題】本発明は、従来より産
業廃棄物として廃棄処分していた胚軸から、不純物含量
の少ない状態でオリゴ糖を抽出するという、簡便且つ安
価な方法を提供するものであって、これら産業廃棄物と
して今後ますます問題になる大豆胚軸を有効利用するも
のである。DISCLOSURE OF THE INVENTION The present invention provides a simple and inexpensive method for extracting oligosaccharides from hypocotyls, which have been conventionally disposed of as industrial wastes, in a state of low impurity content. However, the soybean hypocotyl, which will become more and more problematic as these industrial wastes, will be effectively utilized.
【0007】[0007]
【課題を解決するための手段】本発明者は、如上の点に
鑑み鋭意検討した結果、従来より廃棄処分されるか或い
は飼料、肥料程度にしか使用されなかった大豆胚軸か
ら、あるpH領域でその中に含有される蛋白質が沈殿不溶
化されることを利用し、本発明を完成するに到った。Means for Solving the Problems As a result of intensive studies in view of the above points, the present inventor has found that a soybean hypocotyl, which has been conventionally disposed of or used only for feed or fertilizer, has a certain pH range. Thus, the present invention has been completed by utilizing the fact that the protein contained therein is insolubilized by precipitation.
【0008】即ち本発明は、大豆種子の胚軸を原料と
し、これをpH3乃至6の酸性水溶液下に混合・攪拌し
て、ラフィノース、スタキオース等のオリゴ糖を抽出す
ることを特徴とする、ガラクトオリゴ糖の調製法、であ
る。That is, the present invention uses a soybean seed hypocotyl as a raw material, and mixes and stirs this in an acidic aqueous solution having a pH of 3 to 6 to extract oligosaccharides such as raffinose and stachyose. A method for preparing sugar.
【0009】本発明調製法の概略について記すと、大豆
より分離した胚軸を粉砕後、脱脂を行い脱脂胚軸を得
る。この脱脂に使用される溶剤はヘキサンなど一般に食
用油脂の抽出に使用される溶剤であればどんな溶剤でも
良く、特に限定される物ではない。The outline of the preparation method of the present invention will be described. After crushing the hypocotyl separated from soybean, defatting is performed to obtain a defatted hypocotyl. The solvent used for this degreasing may be any solvent that is generally used for extracting edible oils and fats such as hexane, and is not particularly limited.
【0010】このようにして得た脱脂胚軸を、pH3乃至
6好ましくは4乃至5の酸性水溶液下に混合・攪拌す
る。水溶液のpH値が上記範囲を逸脱すると、抽出液中の
不純物量が増加するので、好ましくない。The defatted hypocotyl thus obtained is mixed and stirred in an acidic aqueous solution of pH 3 to 6, preferably 4 to 5. If the pH value of the aqueous solution deviates from the above range, the amount of impurities in the extract increases, which is not preferable.
【0011】混合に際し、混合液のpH値が3乃至6好ま
しくは4乃至5になる様に、予め塩酸などの酸を加えて
pH調製した酸溶液を混合するのが好ましい。During the mixing, an acid such as hydrochloric acid is added in advance so that the pH value of the mixed solution becomes 3 to 6, preferably 4 to 5.
It is preferred to mix the pH adjusted acid solution.
【0012】混合する水溶液の量は、脱脂胚軸に対して
4倍程度が好ましい。なお、水溶液の量が少ないと、後
の乾燥工程でその操作が簡略化できる一方、抽出時の攪
拌或いは抽出液の分離が難しくなる。逆に、水溶液の量
が多いと、攪拌がし易く抽出効率及び分離時の収量が増
すが、乾燥工程で除去する水の量が多くなる為、コスト
が掛かる。従って、混合する水溶液の量はこれらの状況
を加味した上で適宜決定すればよい。The amount of the aqueous solution to be mixed is preferably about 4 times the defatted hypocotyl. If the amount of the aqueous solution is small, the operation can be simplified in the subsequent drying step, but it becomes difficult to stir during extraction or separate the extract. On the other hand, when the amount of the aqueous solution is large, stirring is easy and the extraction efficiency and the yield at the time of separation are increased, but the amount of water to be removed in the drying step is large, resulting in cost increase. Therefore, the amount of the aqueous solution to be mixed may be appropriately determined in consideration of these situations.
【0013】抽出工程時の温度は、20℃乃至80℃好まし
くは40℃乃至60℃が適当である。余り低温過ぎるとその
抽出効率が低下し、逆に高温過ぎるとその抽出効率が向
上するが、糖とアミノ酸による褐変或いはオリゴ糖の加
水分解が起こるので上記温度範囲が好ましい。The temperature during the extraction step is 20 ° C to 80 ° C, preferably 40 ° C to 60 ° C. If the temperature is too low, the extraction efficiency is lowered, and if the temperature is too high, the extraction efficiency is improved. However, the browning or oligosaccharide hydrolysis by sugars and amino acids occurs, and therefore the above temperature range is preferable.
【0014】以上の条件で抽出する事により不純物であ
る蛋白質の多くは沈殿する。この工程の後に遠心分離或
いは濾過など適当な手段によって固液分離を行い、オリ
ゴ糖抽出液を得る。このようにして得た抽出液は、蛋白
質が少なく高濃度のオリゴ糖含有液である。また、この
沈殿した蛋白質には沈殿時に蛋白と挙動を同じくする物
質が多く含まれ、より不純物を含まないオリゴ糖が抽出
されるのである。By extracting under the above conditions, most of the proteins as impurities are precipitated. After this step, solid-liquid separation is performed by an appropriate means such as centrifugation or filtration to obtain an oligosaccharide extract. The extract thus obtained is a liquid containing a small amount of protein and having a high concentration of oligosaccharide. In addition, the precipitated protein contains a large amount of substances that behave similarly to the protein during precipitation, and oligosaccharides containing less impurities are extracted.
【0015】[0015]
【実施例】以下、実施例を例示して本発明の効果をより
一層明瞭にするが、これは例示であって本発明の精神が
これらの例示によって制限されるものではない。なお、
例中に示す部、%は何れも重量基準を意味する。EXAMPLES Hereinafter, the effects of the present invention will be further clarified by exemplifying examples, but this is an example and the spirit of the present invention is not limited by these examples. In addition,
All parts and% in the examples mean weight basis.
【0016】実施例1〜7、比較例1〜3 脱脂大豆胚軸 100部に、下表に示すそれぞれのpHを有す
る酸性水溶液 400部を加え、室温で1時間攪拌抽出を行
った後に、遠心分離(10000G,20min)を行い、抽出液を分
離した。この酸性抽出液を水酸化ナトリウムを用いて中
和した後、乾燥して抽出物を得た。この抽出物の性状は
以下のとおり。Examples 1 to 7 and Comparative Examples 1 to 100 parts of defatted soybean hypocotyl were added 400 parts of an acidic aqueous solution having each pH shown in the table below, and the mixture was subjected to stirring extraction at room temperature for 1 hour and then centrifuged. Separation (10000 G, 20 min) was performed to separate the extract. The acidic extract was neutralized with sodium hydroxide and then dried to obtain an extract. The properties of this extract are as follows.
【0017】 表−1 ──────────────────────────────────── 実験 抽出 収率 灰分 粗蛋白 全糖量 ラフィノ スタキオ No. pH (%) (%) (%) (%) ース(%) ース(%) ──────────────────────────────────── 1 1.0 50.3 11.3 50.6 29.8 4.17 19.7 2 2.0 45.5 10.5 47.3 32.9 5.10 22.7 3 3.0 42.6 8.7 20.5 55.8 9.14 38.0 4 3.5 40.3 8.6 18.4 58.0 9.74 40.7 5 4.0 38.6 5.2 16.3 63.0 10.4 44.5 6 4.5 37.2 5.1 15.2 64.1 10.9 45.0 7 5.0 36.8 4.2 20.5 61.0 10.1 42.7 8 5.5 40.2 4.5 23.0 58.1 9.37 41.2 9 6.0 47.2 3.5 50.7 37.0 6.19 26.3 10 7.0 50.3 3.5 61.4 29.7 3.89 16.9 ────────────────────────────────────Table-1 ──────────────────────────────────── Experiment Extraction Yield Ash Content Crude Protein Total Sugar amount Rafino Stacchio No. pH (%) (%) (%) (%) Sose (%) Sose (%) ────────────────────── ─────────────── 1 1.0 50.3 11.3 50.6 29.8 4.17 19.7 2 2.0 45.5 10.5 47.3 32.9 5.10 22.7 3 3.0 42.6 8.7 20.5 55.8 9.14 38.0 4 3.5 40.3 8.6 18.4 58.0 9.74 40.7 5 4.0 38.6 5.2 16.3 63.0 10.4 44.5 6 4.5 37.2 5.1 15.2 64.1 10.9 45.0 7 5.0 36.8 4.2 20.5 61.0 10.1 42.7 8 5.5 40.2 4.5 23.0 58.1 9.37 41.2 9 6.0 47.2 3.5 50.7 37.0 6.19 26.3 10 7.0 50.3 3.5 61.4 29.7 3.89 16.9 ───── ───────────────────────────────
【0018】(注)分析値は全て乾物当たりの%。但
し、灰分は600 ℃強熱残渣分として、粗蛋白質はケルダ
ール法、全糖量はフェノール硫酸法、それぞれのオリゴ
糖は高速液体クロマトグラフィーを用いて測定した(カ
ラムはアサヒパックNH2P-50 、溶出液はアセトニトリ
ル:水=85:15、検出器は日本分光830RI 、流量は0.5m
l/min にて測定) 。(Note) All analytical values are% per dry matter. However, the ash content was measured at 600 ° C as an ignition residue, the crude protein was measured by the Kjeldahl method, the total sugar amount was measured by the phenol-sulfuric acid method, and each oligosaccharide was measured by high performance liquid chromatography (column: Asahi Pack NH2P-50, elution Liquid is acetonitrile: water = 85: 15, detector is JASCO 830RI, flow rate is 0.5m.
(Measured at l / min).
【0019】上表の結果から明らかなように、脱脂大豆
胚軸よりpH3乃至6の酸性水溶液でオリゴ糖を抽出する
とその抽出物中の蛋白質が少なく、中和時の灰分の生成
も少なくて、逆に全糖量は多く、特にラフィノースおよ
びスタキオース含量が高い(実験 No.3〜9)。以上に
対し、中性域或いはpH2以下という強酸性下で抽出する
と、抽出物中の灰分および粗蛋白の生成が多く不純物の
量が多い(実験 No.1〜2,10) 。なお、実験 No.3〜
9はそれぞれ実施例1〜7であり、実験 No.1〜2,10
はそれぞれ比較例1〜3である。As is clear from the results in the above table, when oligosaccharides were extracted from the defatted soybean hypocotyl with an acidic aqueous solution of pH 3 to 6, the extract contained less protein and produced less ash during neutralization. On the contrary, the total sugar amount is large, and especially the raffinose and stachyose contents are high (Experiment Nos. 3 to 9). On the other hand, when the extract is extracted in the neutral region or under a strong acidity of pH 2 or less, the ash content and the crude protein in the extract are large and the amount of impurities is large (Experiment Nos. 1-2 and 10). Experiment No. 3 ~
9 are Examples 1 to 7, respectively, and Experiment Nos. 1 to 2 and 10
Are Comparative Examples 1 to 3, respectively.
【0020】以上の如く、本発明調製法によれば、爾後
の精製に使用する薬剤或いは時間が他の抽出物に比較し
て節約されるのである。As described above, according to the preparation method of the present invention, the drug or time used for the subsequent purification can be saved as compared with other extracts.
【0021】実施例8 前例の実験 No.6において、使用する酸として硫酸を用
い、中和時のアルカリ剤として水酸化カルシウムを用い
た。その後に、遠心分離(10000G,20min)を行い、乾燥後
前例と同様の分析を行った。Example 8 In Experiment No. 6 of the previous example, sulfuric acid was used as the acid used and calcium hydroxide was used as the alkaline agent at the time of neutralization. After that, centrifugation (10000 G, 20 min) was performed, and after drying, the same analysis as in the previous example was performed.
【0022】結果は以下のとおり。なお、比較のため前
例の実験 No.10(抽出時のpH7、中和に水酸化ナトリウ
ムを使用)および実験 No.6(抽出時に塩酸を使用、中
和に水酸化ナトリウムを使用)の結果を併記。The results are as follows. For comparison, the results of Experiment No. 10 (pH 7 during extraction, sodium hydroxide used for neutralization) and Experiment No. 6 (hydrochloric acid used during extraction, sodium hydroxide used for neutralization) were compared for comparison. Also written.
【0023】 表−2 ──────────────────────────────────── 実験 抽出 収率 灰分 粗蛋白 全糖量 ラフィノ スタキオ No. pH (%) (%) (%) (%) ース(%) ース(%) ──────────────────────────────────── 10 7.0 50.3 3.5 61.4 29.7 3.89 16.9 6 4.5 37.2 5.1 15.2 64.1 10.9 45.0 11 4.5 36.6 4.2 12.5 69.3 11.7 48.5 ───────────────────────────────────Table-2 ──────────────────────────────────── Experiment Extraction Yield Ash Content Crude Protein Total Sugar amount Rafino Stacchio No. pH (%) (%) (%) (%) Sose (%) Sose (%) ────────────────────── ─────────────── 10 7.0 50.3 3.5 61.4 29.7 3.89 16.9 6 4.5 37.2 5.1 15.2 64.1 10.9 45.0 11 4.5 36.6 4.2 12.5 69.3 11.7 48.5 ─────────── ────────────────────────
【0024】以上の結果、pH調整に硫酸を用い中和に水
酸化カルシウムを用いると、中和塩が沈殿し、抽出物中
に含まれる灰分が少なく、更に、カルシウムによる蛋白
質の沈殿も同時に生成され、より高純度な抽出物が得ら
れた(実験 No.11) 。なお、実験 No.11は実施例8であ
る。As a result, when sulfuric acid is used for pH adjustment and calcium hydroxide is used for neutralization, the neutralized salt precipitates, the ash content contained in the extract is small, and the precipitation of protein due to calcium is also produced at the same time. And a higher-purity extract was obtained (Experiment No. 11). Experiment No. 11 is Example 8.
【0025】以上の結果により、pH調整に硫酸を用いる
と不純物が少なくなるため、爾後の工程が簡略化し精製
に使用する薬剤量が減量出来るのが明らかである。From the above results, it is clear that when sulfuric acid is used for pH adjustment, impurities are reduced, so that the subsequent steps are simplified and the amount of drug used for purification can be reduced.
【0026】[0026]
【発明の効果】本発明により、従来より産業廃棄物とし
て廃棄処分されていた大豆胚軸から、不純物含量の少な
い状態でオリゴ糖を抽出するという、簡便且つ安価な方
法を提供することが可能となったのであり、これら産業
廃棄物として今後ますます問題になる大豆胚軸を有効利
用し得るという効果を有するのである。そして、本発明
は、従来法の如く、豆乳からオリゴ糖を抽出するよりは
抽出液中に存在する蛋白質が極めて少なく、従って精製
時に使用される塩化カルシウム等の蛋白質凝固剤の量が
かなり減量でき、またpH調整に使用する酸として硫酸を
使用した場合、中和にカルシウム等中和塩が水不溶性の
物を生成するアルカリを使用することにより後の脱塩工
程で使用するイオン交換樹脂などの薬剤量が減量でき
る。以上の工程は、アルコール濃縮大豆蛋白ホエイ液か
ら分離精製する時に必要となるエタノールの回収操作が
不必要なために、アルコール濃縮大豆蛋白ホエイからオ
リゴ糖を調製するよりはその工程が簡略になるという効
果を有するのである。EFFECTS OF THE INVENTION According to the present invention, it is possible to provide a simple and inexpensive method for extracting oligosaccharides from soybean hypocotyls, which have been conventionally discarded as industrial wastes, in a state where the content of impurities is low. Therefore, it has the effect of effectively utilizing soybean hypocotyls, which will become more and more problematic as these industrial wastes in the future. And, the present invention, as in the conventional method, has much less protein present in the extract than the extraction of oligosaccharides from soymilk, and therefore the amount of protein coagulants such as calcium chloride used during purification can be considerably reduced. In addition, when sulfuric acid is used as an acid used for pH adjustment, by using an alkali that produces a water-insoluble substance such as a calcium-neutralizing salt for neutralization, ion-exchange resin etc. used in the subsequent desalting step The amount of drug can be reduced. The above steps are simpler than those for preparing oligosaccharides from alcohol-enriched soy protein whey, because the ethanol recovery operation required when separating and purifying from alcohol-enriched soy protein whey is unnecessary. It has an effect.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 服部 光男 茨城県北相馬郡守谷町松前台4−2−3 A−207 (72)発明者 栗田 博子 茨城県北相馬郡守谷町松前台1−12−1 (72)発明者 武井 千恵美 茨城県北相馬郡守谷町松前台1−12−4 (72)発明者 佐藤 陽子 茨城県筑波郡谷和原村絹の台5−7−1 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Mitsuo Hattori 4-2-3 Matsumaedai, Moriya-cho, Kitasoma-gun, Ibaraki A-207 (72) Hiroko Kurita 1-12 Matsumae-dai, Moriya-cho, Kitasoma-gun, Ibaraki -1 (72) Inventor Chiemi Takei 1-12-4 Matsumaedai Moriya-cho, Kitasoma-gun, Ibaraki Prefecture Inventor Yoko Yoko Sato 5-7-1 Kinnodai, Yawahara-mura, Tsukuba-gun, Ibaraki Prefecture
Claims (1)
乃至6の酸性水溶液下に混合・攪拌して、ラフィノー
ス、スタキオース等のオリゴ糖を抽出することを特徴と
する、ガラクトオリゴ糖の調製法。1. A soybean seed hypocotyl is used as a raw material, which is adjusted to pH 3
A method for preparing a galacto-oligosaccharide, which comprises mixing and stirring in an acidic aqueous solution of Nos. 6 to 6 to extract oligosaccharides such as raffinose and stachyose.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3321383A JPH05123200A (en) | 1991-11-07 | 1991-11-07 | Preparation of galactooligosaccharide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3321383A JPH05123200A (en) | 1991-11-07 | 1991-11-07 | Preparation of galactooligosaccharide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH05123200A true JPH05123200A (en) | 1993-05-21 |
Family
ID=18131946
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3321383A Pending JPH05123200A (en) | 1991-11-07 | 1991-11-07 | Preparation of galactooligosaccharide |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH05123200A (en) |
-
1991
- 1991-11-07 JP JP3321383A patent/JPH05123200A/en active Pending
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